US4116759A - Preparation of liquor for delignification or alkali treatment by autocaustization, and the preparation of pulp with this liquor - Google Patents
Preparation of liquor for delignification or alkali treatment by autocaustization, and the preparation of pulp with this liquor Download PDFInfo
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- US4116759A US4116759A US05/719,139 US71913976A US4116759A US 4116759 A US4116759 A US 4116759A US 71913976 A US71913976 A US 71913976A US 4116759 A US4116759 A US 4116759A
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- alkaline
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- bleaching
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1068—Bleaching ; Apparatus therefor with O2
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/04—Pulping cellulose-containing materials with acids, acid salts or acid anhydrides
Definitions
- insoluble calcium carbonate is also formed (lime sludge), which is usually separated, heated (lime sludge reburning), until it has been transformed into calcium oxide and is then dissolved into new calcium hydroxide.
- lime sludge insoluble calcium carbonate
- Caustisation requires both equipment and time, and if it could be avoided this would mean a considerable saving for a pulp mill.
- the present invention is intended to eliminate the caustisation by addition of a chemical and separation of a byproduct, as used in the past. This can be achieved by the use of chemicals other than the conventional ones by alkaline pulping processes. Since alkali is required also for the bleaching of pulp, conventional bleaching alkali can be substituted by chemicals, which can be regenerated according to the present invention.
- Another advantage in cooking and bleaching with these chemicals is, that a more even pH value is obtained, and thereforeless carbohydrate degradation.
- the chemicals can be used for alkali treatment of pulp that has already been made, for example, in connection with viscose preparation.
- Such liquor can be prepared according to the invention.
- FIG. 1 is a graphic illustration of the completeness of caustisation of a given borate-carbonate ratio at different temperatures
- FIG. 2 is a graphic illustration showing the completeness of caustisation of various molar ratios of borates and phosphates.
- FIG. 3 is a graphic illustration showing the completeness of caustisation of various molar ratios of phosphates at different temperatures.
- the caustisation procedure according to the invention will hereinafter be called autocaustisation. It is applicable if use is made of certain salts of polyprotic inorganic acids, such as boric or orthophosphoric acid, as pulping chemicals (or bleaching chemicals -- generally: delignification chemicals).
- pulping chemicals or bleaching chemicals -- generally: delignification chemicals.
- the liquor is evaporated and burnt, whereafter in the main its content of organic matter will have been transformed into carbon dioxide and water, whereby part of the carbon dioxide will be bound in the form of carbonate to the non-volatile residue ("ash” or "melt", depending upon the temperature).
- ash non-volatile residue
- the carbon dioxide is expelled from the carbonate without the addition of a separate chemical.
- the alkali where the Na 2 HBO 3 and alkali-consuming organic matter in the cook, such as lignin, by LignOH.
- the principle of autocaustisation is based on the fact that one can expel the carbon dioxide from carbonate with an acid, H 2 BO 3 , which is weaker than carbon dioxide, provided one or several reaction products (in this case CO 2 and H 2 O) are removed from the system.
- the equilibrium in reaction 3 may thus be inclined to the left, but since CO 2 and H 2 O are allowed to leave continuously, the product Na 2 HBO 3 can be obtained in a theoretical yield.
- the cooking chemical in both its uncausticised and its causticised form NaH 2 BO 3 and Na 2 HBO 3 , resp
- the causticised product Na 2 HBO 3 is sufficiently alkaline, it is usable as a delignification chemical. This is the case with secondary sodium borate, Na 2 HBO 3 , which has been shown approximately to correspond equimolarly to NaOH as effective alkali during alkaline pulping.
- the salt Na 2 HBO 3 does not exist as such in a dry state, but dehydrated, viz. according to the formula:
- Na 2 HBO 3 and generally Na m+1 H n-1 A, are also allowed to represent such salts of corresponding polynuclear ions.
- the borate salt is used in a concentration of 0.1 to 2.0 mols of boron/liter so that during the pulping or bleaching process 0.2 to 2.0 mols of hydroxyl ions per mol of boron are liberated through hydrolysis of the salt.
- the borate in the residual liquor has a molar ratio of Na:B of 1 - 2 (excluding Na present as Na 2 S) and is combusted at a temperature of 200° l C. to 1500° C., with dissolution of the residue in water following.
- T is the absolute temperature in K (Kelvin).
- the energy of activation was 111 kJ/mol, which may for example mean, that the reaction speed is doubled if the temperature is increased from 875° to 947° C.; If the molar ratio F varies, it is obvious that it is easy to causticise if F ⁇ 2, but not if F>2 (see FIG. 2). This is also to be expected, since if F>2, the mixture will consist of NaH 2 BO 3 and Na 2 CO 3 , and carbon dioxide can be expected to be expelled by the ion H 2 BO 3 (whereby HBO 3 2- will be formed), but not by the ion HBO 3 2- , which is not a sufficiently strong acid.
- the degree of caustisation refers to that part of the carbonate formed during combustion which has expelled its CO 2 during heating.
- Both kraft and "soda” cooking can be done with borate or phosphate instead of hydroxide as alkali, as can bleaching, for instance oxygen bleaching.
- the following oxygen bleaching experiments may be presented as examples of the use of weakly-alkaline NaH 2 BO 3 .
- the starting material was birch alkali pulp, cooked to the yield 67.4%, and with lignin content 21.7%.
- the pulp consistency was 10%, the oxygen pressure 8 bar, the maximum temperature 120° C. and the time at 120° C. 45 min.
- alkaline borate such as Na 2 HBO 3
- hydroxide instead of hydroxide
- Alkali losses during the pulping cycle may be covered by borax and soda.
- bleaching alkali may be prepared, and also analogously, other inorganic chemicals may be used.
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
A method for the regeneration of pulping or bleaching chemicals from spent liquor containing salts of polybasic organic acids. The liquor is evaporated and then burned so that organic matter will be discharged as carbon dioxide and water, and a carbonate residue is formed. Carbon dioxide is expelled from the carbonate with an acid by autocaustization to regenerate the cooking chemicals.
Description
When alkaline spent pulping liquors are burnt to yield chemicals and heat, one of the main products is sodium carbonate. In the case of black liquor from kraft cooks, sodium sulfide will also be formed. The product is dissolved in water into so-called green liquor after the passage through the recovery furnace. As a rule, the carbonate is usually not sufficiently alkaline to pulp wood or similar fibrous material to an adequate degree. The carbonate is consequently transformed into hydroxide. This process is called caustisation, and is conducted with the aid of a metal hydroxide solution, of which the corresponding carbonate has a low solubility in water. In practice, calcium hydroxide is used for the caustisation. In addition to soluble sodium hydroxide, insoluble calcium carbonate is also formed (lime sludge), which is usually separated, heated (lime sludge reburning), until it has been transformed into calcium oxide and is then dissolved into new calcium hydroxide. Caustisation requires both equipment and time, and if it could be avoided this would mean a considerable saving for a pulp mill.
The present invention is intended to eliminate the caustisation by addition of a chemical and separation of a byproduct, as used in the past. This can be achieved by the use of chemicals other than the conventional ones by alkaline pulping processes. Since alkali is required also for the bleaching of pulp, conventional bleaching alkali can be substituted by chemicals, which can be regenerated according to the present invention.
Another advantage in cooking and bleaching with these chemicals is, that a more even pH value is obtained, and thereforeless carbohydrate degradation.
In addition, the chemicals can be used for alkali treatment of pulp that has already been made, for example, in connection with viscose preparation. Also such liquor can be prepared according to the invention.
The drawings illustrate the best mode presently contemplated of carrying out the invention.
In the drawings:
FIG. 1 is a graphic illustration of the completeness of caustisation of a given borate-carbonate ratio at different temperatures;
FIG. 2 is a graphic illustration showing the completeness of caustisation of various molar ratios of borates and phosphates; and
FIG. 3 is a graphic illustration showing the completeness of caustisation of various molar ratios of phosphates at different temperatures.
The caustisation procedure according to the invention will hereinafter be called autocaustisation. It is applicable if use is made of certain salts of polyprotic inorganic acids, such as boric or orthophosphoric acid, as pulping chemicals (or bleaching chemicals -- generally: delignification chemicals). After such use, the liquor is evaporated and burnt, whereafter in the main its content of organic matter will have been transformed into carbon dioxide and water, whereby part of the carbon dioxide will be bound in the form of carbonate to the non-volatile residue ("ash" or "melt", depending upon the temperature). At a sufficiently high temperature, the carbon dioxide is expelled from the carbonate without the addition of a separate chemical. In principle. the following three stages can be noticed for the alkali, where the Na2 HBO3 and alkali-consuming organic matter in the cook, such as lignin, by LignOH.
1. cooking or bleaching (delignification):
Na.sub.2 HBO.sub.3 LignOH ⃡ LignONa+NaH.sub.2 BO.sub.3
2. combustion:
2 LignONa+x.O.sub.2 →Na.sub.2 CO.sub.3 +y.CO.sub.2 +z.H.sub.2 O
3. autocaustisation:
2NaH.sub.2 BO.sub.3 +Na.sub.2 CO.sub.3 →2Na.sub.2 HBO.sub.3 +CO.sub.2 +H.sub.2 O
the principle of autocaustisation is based on the fact that one can expel the carbon dioxide from carbonate with an acid, H2 BO3, which is weaker than carbon dioxide, provided one or several reaction products (in this case CO2 and H2 O) are removed from the system. The equilibrium in reaction 3 may thus be inclined to the left, but since CO2 and H2 O are allowed to leave continuously, the product Na2 HBO3 can be obtained in a theoretical yield. However, it should be noted that the cooking chemical in both its uncausticised and its causticised form (NaH2 BO3 and Na2 HBO3, resp) should be non-volatile; it normally is so if it is a sodium salt. If the causticised product Na2 HBO3 is sufficiently alkaline, it is usable as a delignification chemical. This is the case with secondary sodium borate, Na2 HBO3, which has been shown approximately to correspond equimolarly to NaOH as effective alkali during alkaline pulping.
The salt Na2 HBO3 does not exist as such in a dry state, but dehydrated, viz. according to the formula:
2 Na.sub.2 HBO.sub.3 ⃡Na.sub.4 B.sub.2 O.sub.5 +H.sub.2 O
however, by redissolution in water the salt is hydrolysed back to orthoborate. In the subsequent text, Na2 HBO3, and generally Nam+1 Hn-1 A, are also allowed to represent such salts of corresponding polynuclear ions.
The borate salt is used in a concentration of 0.1 to 2.0 mols of boron/liter so that during the pulping or bleaching process 0.2 to 2.0 mols of hydroxyl ions per mol of boron are liberated through hydrolysis of the salt.
The borate in the residual liquor has a molar ratio of Na:B of 1 - 2 (excluding Na present as Na2 S) and is combusted at a temperature of 200° l C. to 1500° C., with dissolution of the residue in water following.
The conditions needed for autocaustisation depend upon the nature of the chemical concerned. As is shown in FIG. 1, one can achieve with a mixture of 2 mol NaH2 BO3 and 1 mol Na2 CO3 (when thus the total molar ratio F = Na:B is equal to 2.0), by heating at 875° C. for 3 h there is attainable a degree of caustisation of 80% (20% CO2 of original amount remaining). Caustisation experiments with the same borate-carbonate mixture have been performed within the temperature interval 725°-875° C. (see FIG. 1) for times between 0 and 3 h 30 min. It appeared that the decomposition of the carbonate approximately followed first order kinetics, and that the reaction constant k (is s-1) could be calculated by means of the equation:
lnk = 2.67 - (13350/T)
where T is the absolute temperature in K (Kelvin). The energy of activation was 111 kJ/mol, which may for example mean, that the reaction speed is doubled if the temperature is increased from 875° to 947° C.; If the molar ratio F varies, it is obvious that it is easy to causticise if F≦2, but not if F>2 (see FIG. 2). This is also to be expected, since if F>2, the mixture will consist of NaH2 BO3 and Na2 CO3, and carbon dioxide can be expected to be expelled by the ion H2 BO3 (whereby HBO3 2- will be formed), but not by the ion HBO3 2-, which is not a sufficiently strong acid.
Analogous experiments with phosphate have shown, that it is possible to perform the following autocaustisation:
2 Na.sub.2 HPO.sub.4 +Na.sub.2 CO.sub.3 →2 Na.sub.3 PO.sub.4 +CO.sub.2 +H.sub.2 O
as is shown in FIG. 3, after about 40 min at 525° C. 80% of the carbon dioxide has been expelled, and at 625°-725° C. as much as 90%. If the molar ratio G = Na:P exceeds 3, caustisation will be incomplete (see FIG. 2); if G≧4, no caustisation will occur. For example, if G = 3.5, the mixture will be causticised half-way (FIG. 3):
na.sub.3 PO.sub.4 +Na.sub.2 HPO.sub.4 +Na.sub.2 CO.sub.3 →2 Na.sub.3 PO.sub.4 +1/2Na.sub.2 CO.sub.3 +1/2CO.sub.2 +1/2H.sub.2 O
thus, for borate - and phosphate liquor it is essential to keep F = Na/B≦2 and G=Na:P≦3, respectively, to ensure complete caustisation. Salts of other amphoteric electrolytes silicates and aluminates, such as might also be used analogously.
Experiments have also been made with organic substance present during the heating of borate- and phosphate salts in the presence of air, to simulate the burning and caustisation of real spent liquors. Thus, Na2 HBO3 and Na3 PO4, respectively, have been mixed with vanilline and glucose (and some water) and heated in a laboratory oven. The caustisation then proceeded a little more slowly than when pure carbonate was present instead of the organic compounds, see Fig. 1.
Examples are given below from experiments with real pulping spent liquors (birch liquors, corresponding to pulp yields of 65-79%):
__________________________________________________________________________
Composition
Theoretical amount
Found amount after
Degree
Main
of original
after combustion of 1 1
combustion and heating
of caus-
product
cooking
spent liquor, mmol
of 1 1 spent liquor, mmol
tisation
after dis-
liquor Na B P CO.sub.2
Na B P CO.sub.2
% solution
__________________________________________________________________________
NaOH 1000
-- -- 500
881
-- -- 283 36 Na.sub.2 CO.sub.3
Na.sub.2 HBO.sub.3
1740
870
-- 435
1686
949
-- 23 95 Na.sub.2 HBO.sub.3
NaBO.sub.3
550
550
-- 0 523
518
-- 3 -- NaH.sub.2 BO.sub.3
Na.sub.3 PO.sub.4
3750
-- 1250
625
3986
-- 1340
76 89 Na.sub.3 PO.sub.4
__________________________________________________________________________
The degree of caustisation refers to that part of the carbonate formed during combustion which has expelled its CO2 during heating.
It is thus obvious that one can burn and regenerate borate- and phosphate spent liquors by heating (autocaustisation) in such a way as to give liquors which are re-usable as alkali for the preparation of pulps.
Both kraft and "soda" cooking can be done with borate or phosphate instead of hydroxide as alkali, as can bleaching, for instance oxygen bleaching.
Examples of birch kraft cooks at a liquor - to - wood ratio of 3.6, and to a H-factor of 981:
______________________________________
Total Degree
yield Screen- of
Cooking chemicals, mol/l
% of ings % Lignin
deligni-
Na.sub.2 S
NaOH Na.sub.2 HBO.sub.3
wood of wood
% fication
______________________________________
0.20 0.98 -- 52.4 0.1 3.8 0.90
0.22 -- 1.14 52.4 0.2 3.1 0.92
______________________________________
An example is given below of "soda" cooks of birch (liquor - to - wood ratio 4.0):
______________________________________
Degree
Total Lig- of
Cooking chemicals, mol/l
H yield % nin deligni-
NaOH Na.sub.2 HBO.sub.3
Na.sub.3 PO.sub.4
factor
of wood
% fication
______________________________________
-- 0.61 -- 533 69.4 21.2 0.29
0.80 -- -- 482 68.1 20.1 0.34
-- -- 1.50 482 69.9 21.0 0.29
______________________________________
From a number of kraft and alkali cooks of birch it has been found, that 1 mol Na2 HBO3 corresponds to 1.2 mol NaOH, and that 1 mol Na3 PO4 corresponds to about 0.5-0.6 mol NaOH during cooking.
The following oxygen bleaching experiments may be presented as examples of the use of weakly-alkaline NaH2 BO3. The starting material was birch alkali pulp, cooked to the yield 67.4%, and with lignin content 21.7%. During the bleaching, the pulp consistency was 10%, the oxygen pressure 8 bar, the maximum temperature 120° C. and the time at 120° C. 45 min.
__________________________________________________________________________
Total Degree Bright-
yield, % of Viscosity
ness
Alkali, mol/l
Final
after
Lignin
deligni-
SCAN SCAN
NaOH
NaH.sub.2 BO.sub.3
pH bleaching
% fication
dm.sup.3 /kg
%
__________________________________________________________________________
0.29
-- 10.9
54.9 11.2
0.70
690 33.0
-- 0.60 9.9
57.0 11.1
0.70
740 32.1
__________________________________________________________________________
In this case the advantage with weak alkali was that at a certain lignin content the yield was about 2 abs. % higher.
According to the invention, it is thus possible to use alkaline borate, such as Na2 HBO3, instead of hydroxide during pulping, and it is also possible, after the organic material in the spent liquor has been burnt into carbonate, to causticise the remainder by heating, so as to obtain new alkaline liquor suitable for use in pulping. Alkali losses during the pulping cycle may be covered by borax and soda. Analogously, bleaching alkali may be prepared, and also analogously, other inorganic chemicals may be used.
Various modes of carrying out the invention are contemplated as being within the scope of the following claims particularly pointing out and distinctly claiming the subject matter which is regarded as the invention.
Claims (8)
1. A method for the alkali pulping of ligno-cellulose materials, comprising the steps of cooking the ligno-cellulose material in an alkaline aqueous cooking liquor containing as an active ingredient at least one alkaline salt of a polybasic inorganic acid selected from the group consisting of NaH2 BO3 and Na2 HBO3, combusting the residual cooking liquor to obtain an alkaline inorganic substance, and dissolving said inorganic substance in water to provide the same alkaline salt as used in the cooking step.
2. The method of claim 1, wherein the polybasic acid is boric acid and the borate salt is used in a concentration of 0.1-2.0 mol B/1 and so that during the pulping process 0.2-2.0 mols of hydroxyl ions per mol of boron are liberated through hydrolysis of the salt.
3. The method of claim 1, wherein the liquor is evaporated prior to combusting.
4. The method of claim 1 wherein the acid is boric acid, and the borate in said residual liquor has a molar ratio Na:B of 1-2 (excluding Na present as Na2 S) and is combusted at a temperature of 200° C. to 1500° C.
5. A method for the alkaline bleaching of pulp derived from ligno-cellulose materials, the steps comprising bleaching the pulp in the presence of oxygen in an aqueous alkaline liquor containing as an active ingredient at least one alkaline salt of a polybasic inorganic acid selected from the group consisting of Na2 HBO3 and NaH2 BO3, combusting the residual liquor to obtain an alkaline inorganic substance, and dissolving the inorganic substance in water to form the same alkaline salt used in the bleaching step.
6. The method of claim 5, wherein the alkaline salt is used in a concentration of 0.1 to 2.0 mols of boron/1 so that during the bleaching process 0.2 to 2.0 mols of hydroxyl ions per mol of boron are liberated through hydrolysis of the salt.
7. The method of claim 5, wherein the liquor is evaporated prior to combustion.
8. The method of claim 5, wherein the alkaline salt in said residual liquor has a molar ratio of Na:B of 1-2 (excluding Na present as Na2 S) and is combusted at a temperature at 200° C. to 1500° C.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI752463A FI53141C (en) | 1975-09-02 | 1975-09-02 | |
| FI752463 | 1975-09-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4116759A true US4116759A (en) | 1978-09-26 |
Family
ID=8509408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US05/719,139 Expired - Lifetime US4116759A (en) | 1975-09-02 | 1976-08-31 | Preparation of liquor for delignification or alkali treatment by autocaustization, and the preparation of pulp with this liquor |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4116759A (en) |
| AU (1) | AU499100B2 (en) |
| BR (1) | BR7605508A (en) |
| CA (1) | CA1087355A (en) |
| FI (1) | FI53141C (en) |
| NO (1) | NO150807C (en) |
| NZ (1) | NZ181792A (en) |
| SE (1) | SE7609675L (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4248662A (en) * | 1979-01-22 | 1981-02-03 | The Black Clawson Company | Oxygen pulping with recycled liquor |
| EP1090181A1 (en) * | 1998-06-01 | 2001-04-11 | U.S. Borax Inc. | Increasing causticizing efficiency of alkaline pulping liquor by borate addition |
| US6294048B1 (en) | 1998-06-01 | 2001-09-25 | U.S. Borax Inc. | Method for regenerating sodium hydroxide by partial autocausticizing sodium carbonate containing smelt by reaction with a borate |
| WO2001088257A1 (en) * | 2000-05-14 | 2001-11-22 | U.S. Borax Inc. | Methods for analyzing boron-containing alkaline pulping liquors |
| WO2003062526A1 (en) * | 2002-01-23 | 2003-07-31 | Rinheat Oy | Method for bleaching mechanically defibered pulp |
| US20050098280A1 (en) * | 2002-09-12 | 2005-05-12 | Lars Stigsson | Alkaline process for the manufacturing of pulp using alkali metaborate as buffering alkali |
| WO2006019342A1 (en) * | 2003-10-09 | 2006-02-23 | Kiram Ab | Partial oxidation of cellulose spent pulping liquor |
| US7494637B2 (en) | 2000-05-16 | 2009-02-24 | Massachusetts Institute Of Technology | Thermal conversion of biomass to valuable fuels, chemical feedstocks and chemicals |
| WO2011020949A1 (en) | 2009-08-18 | 2011-02-24 | M-Real Oyj | Method of producing sodium hydroxide from an effluent of fiber pulp production |
| CN101066516B (en) * | 2007-06-06 | 2011-04-20 | 华东理工大学 | Decarbonizing solution comprising borate |
| CN114763680A (en) * | 2021-01-15 | 2022-07-19 | 中国石油天然气股份有限公司 | Method for removing lignin from lignocellulosic feedstocks |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1643826A (en) * | 1923-12-22 | 1927-09-27 | Bertrand S Summers | Process for making paper pulp |
| US1730383A (en) * | 1929-10-08 | of berlin | ||
| US1868569A (en) * | 1930-07-24 | 1932-07-26 | Kellogg Dils Inc | Method of treating fibers for paper making and other uses |
| US1935580A (en) * | 1930-09-06 | 1933-11-14 | Brown Co | Processing of cellulose fiber |
| US2601110A (en) * | 1945-06-14 | 1952-06-17 | Ontario Paper Co Ltd | Pulping lignocellulose with sodium aluminate |
| US2673148A (en) * | 1950-10-04 | 1954-03-23 | Hercules Powder Co Ltd | Alkaline pulping using gaseous oxygen |
| US3024158A (en) * | 1958-07-02 | 1962-03-06 | Kimberly Clark Co | Manufacture of cellulosic products |
| US3594270A (en) * | 1968-02-02 | 1971-07-20 | Eastman Kodak Co | Upgrading unbleached sulfite pulps |
| US3661699A (en) * | 1970-12-21 | 1972-05-09 | American Cyanamid Co | Bleaching of lignin-containing cellulose materials such as pulp |
-
1975
- 1975-09-02 FI FI752463A patent/FI53141C/fi not_active IP Right Cessation
-
1976
- 1976-08-17 NZ NZ181792A patent/NZ181792A/en unknown
- 1976-08-23 BR BR7605508A patent/BR7605508A/en unknown
- 1976-08-25 AU AU17122/76A patent/AU499100B2/en not_active Expired
- 1976-08-30 NO NO762969A patent/NO150807C/en unknown
- 1976-08-31 US US05/719,139 patent/US4116759A/en not_active Expired - Lifetime
- 1976-09-01 CA CA260,318A patent/CA1087355A/en not_active Expired
- 1976-09-01 SE SE7609675A patent/SE7609675L/en unknown
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1730383A (en) * | 1929-10-08 | of berlin | ||
| US1643826A (en) * | 1923-12-22 | 1927-09-27 | Bertrand S Summers | Process for making paper pulp |
| US1868569A (en) * | 1930-07-24 | 1932-07-26 | Kellogg Dils Inc | Method of treating fibers for paper making and other uses |
| US1935580A (en) * | 1930-09-06 | 1933-11-14 | Brown Co | Processing of cellulose fiber |
| US2601110A (en) * | 1945-06-14 | 1952-06-17 | Ontario Paper Co Ltd | Pulping lignocellulose with sodium aluminate |
| US2673148A (en) * | 1950-10-04 | 1954-03-23 | Hercules Powder Co Ltd | Alkaline pulping using gaseous oxygen |
| US3024158A (en) * | 1958-07-02 | 1962-03-06 | Kimberly Clark Co | Manufacture of cellulosic products |
| US3594270A (en) * | 1968-02-02 | 1971-07-20 | Eastman Kodak Co | Upgrading unbleached sulfite pulps |
| US3661699A (en) * | 1970-12-21 | 1972-05-09 | American Cyanamid Co | Bleaching of lignin-containing cellulose materials such as pulp |
Cited By (25)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4248662A (en) * | 1979-01-22 | 1981-02-03 | The Black Clawson Company | Oxygen pulping with recycled liquor |
| EP1090181A1 (en) * | 1998-06-01 | 2001-04-11 | U.S. Borax Inc. | Increasing causticizing efficiency of alkaline pulping liquor by borate addition |
| US6294048B1 (en) | 1998-06-01 | 2001-09-25 | U.S. Borax Inc. | Method for regenerating sodium hydroxide by partial autocausticizing sodium carbonate containing smelt by reaction with a borate |
| EP1090181A4 (en) * | 1998-06-01 | 2001-10-24 | United States Borax Inc | Increasing causticizing efficiency of alkaline pulping liquor by borate addition |
| US6348128B1 (en) | 1998-06-01 | 2002-02-19 | U.S. Borax Inc. | Method of increasing the causticizing efficiency of alkaline pulping liquor by borate addition |
| US6663749B2 (en) | 1998-06-01 | 2003-12-16 | U.S. Borax Inc. | Method for regenerating sodium hydroxide by partial autocausticizing sodium carbonate containing smelt by reaction with borate |
| US6913672B2 (en) * | 2000-05-14 | 2005-07-05 | U.S. Borax Inc. | Methods for analyzing boron-containing alkaline pulping liquors |
| WO2001088257A1 (en) * | 2000-05-14 | 2001-11-22 | U.S. Borax Inc. | Methods for analyzing boron-containing alkaline pulping liquors |
| US6635147B1 (en) * | 2000-05-14 | 2003-10-21 | U.S. Borax Inc. | Method for analyzing boron-containing alkaline pulping liquors |
| US20040055718A1 (en) * | 2000-05-14 | 2004-03-25 | Hsu Wu-Hwa Wesley | Methods for analyzing boron-containing alkaline pulping liquors |
| AU2001259769B2 (en) * | 2000-05-14 | 2005-10-06 | U.S. Borax Inc. | Methods for analyzing boron-containing alkaline pulping liquors |
| US7494637B2 (en) | 2000-05-16 | 2009-02-24 | Massachusetts Institute Of Technology | Thermal conversion of biomass to valuable fuels, chemical feedstocks and chemicals |
| WO2003062526A1 (en) * | 2002-01-23 | 2003-07-31 | Rinheat Oy | Method for bleaching mechanically defibered pulp |
| US20050098279A1 (en) * | 2002-01-23 | 2005-05-12 | Teemu Tanner | Method for bleaching mechanically defibered pulp |
| US20060124257A9 (en) * | 2002-01-23 | 2006-06-15 | Teemu Tanner | Method for bleaching mechanically defibered pulp |
| US6946057B2 (en) * | 2002-09-12 | 2005-09-20 | Kiram Ab | Alkaline process for the manufacturing of pulp using alkali metaborate as buffering alkali |
| US20050098280A1 (en) * | 2002-09-12 | 2005-05-12 | Lars Stigsson | Alkaline process for the manufacturing of pulp using alkali metaborate as buffering alkali |
| US20060102300A1 (en) * | 2002-09-12 | 2006-05-18 | Lars Stigsson | Alkaline process for the manufacturing of pulp using alkali metaborate as buffering alkali |
| WO2006019342A1 (en) * | 2003-10-09 | 2006-02-23 | Kiram Ab | Partial oxidation of cellulose spent pulping liquor |
| CN101066516B (en) * | 2007-06-06 | 2011-04-20 | 华东理工大学 | Decarbonizing solution comprising borate |
| WO2011020949A1 (en) | 2009-08-18 | 2011-02-24 | M-Real Oyj | Method of producing sodium hydroxide from an effluent of fiber pulp production |
| CN102625778A (en) * | 2009-08-18 | 2012-08-01 | M-真实公司 | Method of producing sodium hydroxide from an effluent of fiber pulp production |
| CN102625778B (en) * | 2009-08-18 | 2015-05-20 | M-真实公司 | Method of producing sodium hydroxide from an effluent of fiber pulp production |
| CN114763680A (en) * | 2021-01-15 | 2022-07-19 | 中国石油天然气股份有限公司 | Method for removing lignin from lignocellulosic feedstocks |
| CN114763680B (en) * | 2021-01-15 | 2024-01-30 | 中国石油天然气股份有限公司 | Method for removing lignin from lignocellulose raw material |
Also Published As
| Publication number | Publication date |
|---|---|
| FI752463A (en) | 1977-03-03 |
| FI53141C (en) | 1978-02-10 |
| NO150807C (en) | 1985-01-02 |
| SE7609675L (en) | 1977-03-03 |
| AU499100B2 (en) | 1979-04-05 |
| BR7605508A (en) | 1977-08-16 |
| CA1087355A (en) | 1980-10-14 |
| NZ181792A (en) | 1979-01-11 |
| AU1712276A (en) | 1978-03-02 |
| FI53141B (en) | 1977-10-31 |
| NO762969L (en) | 1977-03-03 |
| NO150807B (en) | 1984-09-10 |
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Owner name: A. AHLSTROM OSAKEYHTIO, SF-29600 NOORMARKKU, FINLA Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:JANSON, JAN;REEL/FRAME:004275/0608 Effective date: 19840612 |